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The organosolv process for pretreatment and fractionation of lignocellulosic biomass for
fermentation and lignin valorization 6th European Bioethanol Technology Meeting,
Detmold, Germany
Huijgen
W. J. J.; Reith
J. H. & den Uil, H
ECN-L--10-029 MAY 2010
2 ECN-L--10-029
The Organosolv Process for Pretreatment and Fractionation of Lignocellulosic Biomass for Fermentation and Lignin Valorization
Wouter Huijgen, Hans Reith & Herman den Uil
20-04-2010 6th European Bioethanol Technology Meeting, Detmold
Contents
Introduction organosolv• Biomass pretreatment for production second generation bioethanol• Organosolv
Organosolv fractionation at ECN• Experimental
– Process conditions– Enzymatic cellulose hydrolysis– Lignin isolation & characterisation
• Process evaluation
Conclusions
ECN-L--10-029 3
20-04-2010 6th European Bioethanol Technology Meeting, Detmold
Lignocellulose Pretreatment
Production second generation bioethanol from lignocellulose:1. Pretreatment.2. Enzymatic hydrolysis cellulose to glucose.3. Fermentation sugars to bioethanol.
Direct enzymatic saccharification of lignocellulose not feasible:• Structural components strongly linked (physically & chemically).• Cellulose protected against decay by lignin.• Cellulose crystalline.• …
Pretreatment required.
20-04-2010 6th European Bioethanol Technology Meeting, Detmold
Functions Pretreatment
Enhancement enzymatic digestibility of cellulose to fermentable sugars:
• Removing hemicellulose and lignin to improve accessibility for hydrolytic enzymes.
• Removing / altering lignin to reduce non-productive cellulase binding.
• Reducing crystallinity of cellulose.• Creating specific surface area.• ….
Pretreatment: overcoming nature’s protection (biomass ‘recalcitrance’).
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20-04-2010 6th European Bioethanol Technology Meeting, Detmold
Pretreatment Processes
Alternative:• Separation of lignin prior to enzymatic hydrolysis, while preserving the
chemical structure of lignin organosolv.
Several physical-chemical pretreatment routes under development.
Main pretreatment technologies at pilot/demo-scale:• (Dilute) acid pretreatment• Steam explosion
Routes effective for cellulose.
However:• Lignin ends up in residue (with unconverted sugars, process chemicals, ash, etc).• Residue generally only suitable for CHP.
20-04-2010 6th European Bioethanol Technology Meeting, Detmold
Lignin
Lignin (model)
Lignin: • Polymeric network of aromatic compounds.• Potential feedstock for wide range of chemicals and
performance products.• Renewable resource for aromatics!
Wood adhesives and resins
Lignocellulose biorefinery:• No large-scale commercial market for lignin (derivatives)
at the moment (in contrast to sugar derivatives).• Valorisation lignin improves carbon footprint &
economics lignocellulose biorefinery.
ECN-L--10-029 5
20-04-2010 6th European Bioethanol Technology Meeting, Detmold
Lignocellulose Biorefinery
Pretreatment
& fractionation
Lignin
Enzymatichydrolysis
Pretreatment &
fractionation
Lignocellulosicbiomass &
residual streams
Fermentation
Conversion &
synthesis
EthanolButanol
Lactic acidPropanediol
Thermochemicaldepolymerisation& conversion
H/P
Chemical derivatives, e.g. surfactants
Platform chemicals, e.g. phenolics, styrene,…Performance products
Electricity
Heat
Cellulose
Hemi-cellulose
Primary biorefinery Secondary biorefinery
Fuel additives
Pretreatment
& fractionation
Lignin
Enzymatichydrolysis
Pretreatment &
fractionation
Lignocellulosicbiomass &
residual streams
Fermentation
Conversion &
synthesis
EthanolButanol
Lactic acidPropanediol
Thermochemicaldepolymerisation& conversion
H/P
Chemical derivatives, e.g. surfactants
Platform chemicals, e.g. phenolics, styrene,…Performance products
Electricity
Heat
Cellulose
Hemi-cellulose
Primary biorefinery Secondary biorefinery
Fuel additives
20-04-2010 6th European Bioethanol Technology Meeting, Detmold
Organosolv Process
Hemicellulose (derivatives)
Organosolv Lignin separation
Solvent separation
Cellulose (S)(to enzymatic hydrolysis)
Lignin (S)
Solvent recycling
Water (+ catalyst)Organic solventLignocellulose
Many different organic solvents applied:• Alcohols (methanol, ethanol, phenol, ethylene glycol…)• Acetone• Organic acids (formic, acetic, …)• 1,4-Dioxane• ….
6 ECN-L--10-029
20-04-2010 6th European Bioethanol Technology Meeting, Detmold
History Organosolv
Begin 20th century (analytics):• Use organic solvent to separate wood components for analysis.
1970-90’s (organosolv pulping):• Organosolv as environmental-friendly alternative to Kraft pulping for paper making.• Many different processes up to pilot-scale:
– Alcell, ethanol-water pulping of wood (Canada).– Organocell, soda pulping with methanol (Germany).– ASAM, alkaline sulphite-anthraquinone-methanol (Germany).– Acetosolv, acetic acid based cooking (Germany).– Milox, formic acid and peroxyformic acid (Finland).– ….
• Extensive overview provided by E. Muurinen (2000), Organosolv pulping, PhD thesis, Oulu university, Finland.
20-04-2010 6th European Bioethanol Technology Meeting, Detmold
Organosolv Biorefinery Processes
Shift to organosolv as: • Pre-treatment for second generation bioethanol.• Primary biorefinery process.
Current developments:• Organosolv biorefinery processes on pilot-scale.
• Lignol (Canada), solvent = ethanol, feedstock = hardwood + softwood.• Chempolis (Finland), solvent = formic acid, feedstock = non-wood lignocellulose.• CIMV (France), solvent = mixture of formic & acetic acid, feedstock = wheat straw.• ….
• Many alternative routes under development at lab-scale.
ECN-L--10-029 7
20-04-2010 6th European Bioethanol Technology Meeting, Detmold
Contents
√ Introduction on organosolv
Organosolv fractionation at ECN• Experimental
– Process conditions– Enzymatic cellulose hydrolysis– Lignin isolation & characterisation
• Process evaluation
Conclusions
20-04-2010 6th European Bioethanol Technology Meeting, Detmold
Process Parameters
Parametric studies performed:• Solvents: ethanol & acetone.• Various lignocellulose feedstocks incl cereal straw.
Studied variables:• Particle size• Solvent mixture : solid ratio• Solvent-water ratio• Pretreatment severity:
– Temperature– Reaction time– Acid catalysts such as H2SO4
• Stirring rate
Afte
rorg
anos
olv
Fres
h w
heat
stra
w
Example: acetone-based organosolv on wheat straw (without catalyst).
8 ECN-L--10-029
20-04-2010 6th European Bioethanol Technology Meeting, Detmold
Experimental Set-up Organosolv Fractionation
Lignocellulose
Filtration
Milling
Solid residue
Filtrate
Washing
Optional:catalyst
Lignin separation & analysis
Analysis composition
Enzymatic hydrolysis
Analysis sugars (monomeric + oligomeric)
Analysis other compounds
Solvent / H2O
Volume: 0.5 / 2 ltrStirringTemperature ↑
T reactor
T jacket
p
0 tt
T p
T reactor
T jacket
0 t
20-04-2010 6th European Bioethanol Technology Meeting, Detmold
Acetone-Water Mixture
Fractionation:
• Organosolv fractionation effective.
• Cellulose recovery >90%.
Acetone:water ratio:
• Strong influence on hemicellulose hydrolysis & delignification.
• Optimisation dependent on product revenues.
0
20
40
60
80
100
0:100 25:75 40:60 50:50 60:40
Acetone-water (% w/w)
Rec
over
ed in
sol
id fr
actio
n (%
)
CelluloseHemicelluloseLignin
Huijgen et al. (2010), Pretreatment and fractionation of wheat straw by an acetone-based organosolv process, submitted.
ECN-L--10-029 9
20-04-2010 6th European Bioethanol Technology Meeting, Detmold
Pretreatment Severity
Fractionation improves with pretreatment severity (temperature & time).
0
20
40
60
80
100
160 175 190 205 220
Temperature (ºC)
Rec
over
ed in
sol
id fr
actio
n (%
)CelluloseHemicelluloseLignin
Maximum severity limited by:
• Decrease cellulose recovery.
• Degradation reactions product loss & inhibiting effect on fermentation.
Huijgen et al. (2010), Pretreatment and fractionation of wheat straw by an acetone-based organosolv process, submitted.
20-04-2010 6th European Bioethanol Technology Meeting, Detmold
Enzymatic Cellulose Hydrolysis
Organosolv effective pretreatment process:• Strong enhancement enzymatic cellulose hydrolysis (>10x).• Enzymatic digestibility at optimised conditions ~90%.
0
20
40
60
80
100
Fresh 160 175 190 205 220
Temperature (°C)
Enzy
mat
ic d
iges
tibili
ty (%
)
Huijgen et al. (2010), Pretreatment and fractionation of wheat straw by an acetone-based organosolv process, submitted.
0
4
8
12
16
20
0 24 48 72
Enzymatic hydrolysis time (h)
[Glu
cose
] (g/
L)
Fresh
220205
190
175
160
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20-04-2010 6th European Bioethanol Technology Meeting, Detmold
Feedstocks
885976Wheat straw
535044Olive tree39
71
92
Enzymatic digestibility (% cellulose feedstock)
5780Barley straw
33Spruce
6450Willow
28Poplar
Delignification (%)
Xylan hydrolysis (%)
Biomass
200 °CEtOH-H2O 60:40% w/w
Effectiveness organosolv dependent on type of lignocellulosic biomass:
• Organosolv less effective for softwoods and (more dense) hardwoods.
• More severe pretreatment conditions or use of catalyst required.
• Organosolv especially suitable for straws.
Stra
wW
illow
PretreatedFresh
20-04-2010 6th European Bioethanol Technology Meeting, Detmold
Lignin Isolation & Characterisation
Lignin isolation:• Insoluble in H2O, soluble in ethanol & acetone.• Precipitation lignin from organosolv liquor.• Lignin isolation efficiency >90%.
160, 180, 200, 220 °C
0
20
40
60
80
100
- 20 40 60 80 100
Solvent composition [wt% organic solvent]
Part
lign
in d
isso
lved
[%]
EthanolAcetoneDioxane
Lignin appearance:• Light brown to black (compacted) powder.• Colour and structure dependent on process conditions
organosolv, biomass type and contaminants.
Lignin purity:• High purity (>90 wt%, up to 96% for wheat straw
derived lignin without additional processing).• Main contaminant oligomeric xylose (hemicellulose).• Lignin sulphur and ash free (max 0.1 wt% S).
ECN-L--10-029 11
20-04-2010 6th European Bioethanol Technology Meeting, Detmold
Lignin Characterisation - II
Molecular weight:• Low mean molecular weight (2000-3500) compared to other types of lignins.• Relatively narrow distribution.
Organosolv lignin promising properties for valorisation (relative to other types of lignin).
Organosolv lignin
31P-NMR:• Identification of functional groups.• SGH type lignins in different ratios depending on feedstock.
20-04-2010 6th European Bioethanol Technology Meeting, Detmold
Simulation Organosolv Process
Process design in ASPEN: • Determination of streams and
energy consumption.• Feedstock: wheat straw.• Process: 200 °C, 60 min,
EtOH:H2O 60:40, 5 L/kg straw.• Preliminary results.
C5 sugars
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20-04-2010 6th European Bioethanol Technology Meeting, Detmold
Recycling Ethanol
Simulations:• Recycling degree ethanol set at 99.9%.• Separation and recycling of ethanol present in moisture cellulose and lignin required!
Benefits using ethanol as solvent:• Solvent = product!• Ethanol in cellulose and hemicellulose streams not directly lost.• Recycling required to avoid product inhibition during fermentation.• Recycling degree might be slightly lowered to save costs.
Importance recycling:• 1 ton wheat straw 0.32 ton EtOH (maximum).• Solvent: 2.7 ton EtOH/ton straw.• Recycling degree 99% 8% EtOH production loss!
20-04-2010 6th European Bioethanol Technology Meeting, Detmold
Energy Consumption
200
83
78-102
3250
41
Temperatures (°C)
Major energy consumers:• Ethanol separation for
recycling.• Large differences in process
temperatures heating.
Heat flows significant compared to energy content ethanol produced.
Next step:• Improved process lay-out including direct recycling of liquor.
ECN-L--10-029 13
20-04-2010 6th European Bioethanol Technology Meeting, Detmold
Recycling Organosolv Liquor
0
20
40
60
80
100
I II III
Recycling step
Rec
over
y in
sol
id fr
actio
n (%
)0
20
40
60
80
100
Glu
cose
yie
ld (%
)
Cellulose Hemicellulose Lignin Enzymatic digestibility
Wheat straw pulping in ethanol.
pH decrease due to recycling acetic acid.
Benefits recycling:• Improvement hemicellulose
hydrolysis.• Substantial increase enzymatic
hydrolysis.
On the other hand:• Increase degradation
hemicellulose sugars.• Slight decrease cellulose recovery.
20-04-2010 6th European Bioethanol Technology Meeting, Detmold
Conclusions
Conclusions:• Organosolv able to fractionate lignocellulose.• Enzymatic hydrolysis cellulose improved substantially (up to ~90% for wheat straw).• Organosolv particularly effective for straw.• Successful isolation of lignin with high purity (>90%).• Lignin promising properties for production of chemicals and performance products.• Recycling organic solvent crucial process element.
Future plans:• Development continuous organosolv reactor.• Lignin conversion tests.• Solvent integrity and recycling. • Investment and operating costs.
14 ECN-L--10-029
ECN-L--10-029 15
20-04-2010 6th European Bioethanol Technology Meeting, Detmold
Thank you for your attention!
More information:[email protected]
http://www.lignovalue.nl/
This work has been performed with subsidy of the Dutch ministry of Economic Affairs and the European Commission in the context of the projects (2007-2010):
Agentschap NL EOS-LT
http://www.biosynergy.eu/